Method and apparatus for making glass



March 11, 1941. w. s. RENDALL METHOD AND APPAKATUS FOB MAKING GLASS Filed Nov'. 13, 1936 3 Sheets-Steet 1 wMsmm w. s. RENDALL 2.234,605

METHOD AND APPARATUS FOR MAKING GLASS Filed Nov. 15, 19:56 3 Sheets-Sheet 2 March 11,' 1941.

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w, s. RNALL METHOD AND APPARATUS FOR MAKING GLSS 5 Shee Filed Nov. 13, 1936 IIIIIIIIIII/IIIIIIII/I// UNITED VSTATES IPATENT OFFICE METHOD AND APPARATUS FOR MAKING GLAss William Stanley Rendall, Baltimore, Md., assignor to Crown Cork & Seal Company, Inc., Baltimore, Md., a corporation of New York Application November 13, 1936, Serial No. 110,'736

1 Claim. (CI. lihi-36.1)

The present invention relates to an improved relatively small mesh size and intimately mixed. method and apparatus for making glass which Further, Ithave discovered that the reaction with may be employed in the manufacture of bottles the steam is carried out best When the solid maand other containers, sheets, and various glass terials are in the form of a relatively thin layer articles. and, to this end, I produce such 'a layerand 5 It is an object of the invention to provide a continuously treat the same with steam presented method whereby the economies resulting from to the layer from one or opposite sides and while the use of rock salt or sodium chloride as an inthe layer is in continuous motion through the gredient of the glass mixture may be taken adreaction zone. In this manner, not only is a' vantage of to produce a high quality glass. Up speedy reaction accomplished, but, of equal imto the present time, the glass industry uses the portance, a complete reaction, so that the desired relatively expensive soda ash or sodium carbonsilicates of calcium and sodium are formed, as ate for the reason that no satisfactory method well as complex or poly-silicates.

has been devised by which the less costly sodium Inorder to achieve the above result, the mixchloride can be utilized. The difference in cost ture is continuously fed to and through the `reof these raw materials is substantial and the inaction zone in a controlled manner as to both dustry has long sought an available method speed of feed and quantity of feed. In some whereby sodium chloride can be used in a comcases, I preheat the ingredients of the' mixture mercially feasible plant. while they are being moved to the reaction zone.

operation in which (1) reaction of the ingredients ment of the ingredients of the mixture to the re-' for glass making takes place and the reacted mass action zone, they are thoroughly mixed in their either (2) refined into glass or (3) reduced to a finely divided state, the charge is delivered at frit, ground, and then converted into glass. These optimum, potentially reactive conditions.

methods are economically acceptable for all prac- The reaction zone which forms a very desirable tical reasons and in addition a high quality homofeature of this invention is preferably in the form geneous glass is obtained A byproduct resulting of a conical or inclined surface to which the from the reaction of the ingredients is also obpreferably preheated and intimately mixed solid tained. ingredients are continuously fed. Where a -cone An important feature of the invention resides is used, the ingredients are fed to the apex of 30 in accomplishing the reaction of the ingredients the cone and a thin layer is formed thereabout. of the glass in a heating chamber with exclusion Where an inclined surface is used, the ingrediof products of combustion. That is to say, in an ents are fed to substantially the top thereof. In oil or gas fired furnace, opportunity for coneach instance, the thin layer of ingredients is tamination of the reaction byproduct or product permitted to move downwardly, while undergoing 5 is eifectively prevented. This result is achieved reaction, and in this connection, the speed of by conducting the reaction between the glass inmovement is such that at the temperature pregredients at the desired temperature, by convailing, complete reaction will take place. Moreduction and radiation, as distinguished from diover, thisspeed of movement downwardly on the rect firing. conical 'or inclined surface is controlled by the 40 Another feature of the invention consists in feed and/or by feeding means associated with the carrying out the reaction under conditions to reaction chamber, so as to reduce the possibility maintain the temperature substantially conof the carrying down of uncombined sodium stant. This result is likewise obtained through chloride,

heating by radiation and conduction and also by During the reaction, as previously stated, steam excluding the reaction zone from any detrimental is diseharged upon, into and through the thin efiects produced, for example, by its proximity to layer of the solid ingredients in their highly and either products of combustion or to the highly intimately mixed state and, while the layer is heated, previously reacted batch, whether in continuously moving at the predetermined speed. solid, molten or semi-molten state. The steam is introduced in such a manner so as I have particularly in mind a glass produced to provide substantially an atmosphere enclosing by the reaction of sand, sodium chloride, calcium the reactive mass and under the temperature carbonate and steam. In order to thoroughly conditions prevailing will assure intimate, compromote this reaction, I have discovered that the plete and rapid reaction.

I have discovered a very simple method of This hastens reaction, and since in the move solid particles must be in a granular form of As heretofore stated, the reaction zone is sub- 5 I stantially segregated from products of combustion or other contaminating influences, as well as high temperature conditions such as might be impressed upon the charge through proximity or direct exposure to a high temperature molten bath of the reacted mass. In addition, this segregation enables the hydrogen chloride gas developed by the reaction to be efliciently removed and recovered and adds an additional economy to the operation, in that either the acid, or free chlorine, is obtained as a commercially usable byproduct. p

The reacted mass as it leaves the reaction zone is usually plastic, i. e;, molten or semi-molten.

` Immediately the reacted mass passes from the reaction zone, it may be subjected to several Operations. For example, (1) the reacted mass is introduced to a high temperature bath (2400 F.) of the previously reacted material and in that manner is rendered fluid, (2) the reacted mass may be immediately and continuously cooled from its plastic state to the form of a frit, (3) the reacted mass may be subjected to an elevated temperature to increase its plasticity or fluidity and (4) the reacted mass, if suiclently plastic or after having its plasticity increased, is suitably molded into bricks, blocks and, in fact, any desired form to produce a vitreous article possessing, by reason of its porosity, useful properties as an acoustic or insulation material.

Where the reacted mass is caused to assume a fluid state by introduction into a molten bath of the previously reacted material, the contents of the bath are continuously drawn off and cooled, in which state the product has a substantially vitreous or frit-like character. Instead of cooling be availed of in a manner to allow it to be molded the bath, however, its plasticity and fiuidity may as above described. Also, the reacted mass in molten or semimolten condition as it leaves the reaction chamber, is immediately cooled to a substantially vitreous or rrit-like state.

The vitreous, fritproduct, either as cooled and solidified from the molten bath or as cooled directly from the reaction chamber, is suitably ground to such a fineness as will promote homogenization. This ground frit is thereafter treated in the ordinary glass furnace to produce a refined product constituting a high quality homogenized glass.

It is an additional feature of the invention that the reacted mass after being transformed into'a molten bath, is continuously or intermittently heated in a glass iurnace to form complete glass. The heating chamber for preparing and holding the bath is preferably in direct communication with the glass furnace which may form a part thereof. The glass furnace is equipped with forming means so that bottles, sheets and a wide variety of glass articles are directly produced.

Where the plasticity of the reacted mass is availed of, either from the bath or directly from the reaction chamber, with or without additional heating or some further cooling to increase or decrease plasticity for making molded products, as before mentioned, the mass is possessed of numerous pores, bubbles, voids and is generally in an unrened but plastic condition. This product when molded retains the cells, voids and bubble-like imperfe-ctions, so that it is relatively poro-us and the molded product therefore, excellent acoustic and insulation qualities.

The term "reacted mass in this specification is intended to mean the reaction product of the ingredients, in a plastic, or molten or semi-molten p state. The expression "frit" is employed to cover the cooled and solidified reacted mass either from a liquid state or directly from the reacted plastic condition. "Glass" as used means the final rened or complete glass produced by heating the reacted mass, the frit, or a bath of the reacted mass.

The apparatus for carrying out the method of the present invention may, as will be appreciated, take many forms and I have therefore in the drawings illustrated several preierred embodiments which, however, must be understood as being purely illustrative.

Referring to the drawings- Figure-l is a diagrammatic View illustrating one method of carrying out the invention.

Fgure 2 is a cross-sectional view through the Figure '7 is an elevation of a further modification of reaction table. v

Figur-e 8 is a section on the line 8-3 of Figure 7, and i Figure 9 is a sectional View of a modified form of reaction furnace.

The ingred'ents of the batch The invention will be described for the manufacture of glass from a typical mixture of ingredients including scdium chloride, calcium carbonate and send, which are reacted in the presence of steam. ,It is tobeunderstood, however, that various types of glass mixtures may be similarly treated in accordance with the method and apparatus of this invention and that the invention is, therefore, 'not limited to the ingredients just recited. Additional ingredients such as feldspar or borax may be added to the mixture for specific purposes, and, in fact innumerable other ingredients may be employed for their recognized purposes in the glass industry. 1

A batch for purposes of illustrating this invention consists of sand (99.8%) 74 pounds, rock salt 9'7.0% sodium chloride) 31 pounds, and raw lime (98.0% calcium carbonate) 18 pounds.

Apparatus Referring to Figure 1, the numeral lil indicates a suitable furnace within which is disposed a chamber H. This chamber is substantially circular and is centrally disposed with respect to the furnace ID. Positioned so as to extend through the wall of the'furnace ll]` are a plurality of burners` or heating units !2, which may be gas flames or oil flames, and these are directecl downwardly and angularly with respect to the 'Wall of the furnace ii), so that the flames are projected tangentially to as distinguished from being directly played upon the wall of the chamber H. The chamber H at its top is provided with a stack or outlet |3 and on its base which is the bottom of the furnace o there is disposed a conical table !4. The table M is provided throughout its length With an opening in which is disposed a 'feeding screw !5. The batch ingredients are supplied to this screw through the conveyor trough !6. Extending inwardly from the wall of chamber I l is a ring-like bafile member !8, the inner diameter of which may be, in some cases, adjustable so as to control the space between the ring and the adjacent conical wall of the table [4. Adjacent its bottom, the wall of the chamber ll is provided with a plurality of openings s which communicate with the bottom of the furnace a and, at one end, the furnace is provided with a suitable outlet 20. Associated with the outlet 23 is a conveyor 2! of any suitable type discharging into a crusher 22 of conventional design and material crushed e therein is discharged upon a suitable table or conveyor 23. Communicating with the chamber I l is a steam outlet 24 and as many thereof may be employed as desired. L

The apparatus described in connection with Figure lis representative of the preferred type of apparatus utilized for carrying out the present invention, but I have developed modifioations thereof which substantially enhance the efiiciency of the method.

Referring to Figure 2, the feed screw !5 is rotated in a tube 5' through the medium of gearing 25. Within the shaft 26 of the feed screw is disposed a steam supply pipe 21. steam is discharged at the top of the conical table l4 through the medium of a plurality of downwardly directed nozzles 28 whose direction is parallel to the surface of the cone, or the steam may be positively directed on the layer carried by the cone. Also, and referring to Figure 3, steam is introduc'ed by pipe 29 within the apex portion 30 of the conical table which is hollowed out, as shown, and forms in efiect a steam chest 3l. The apex portion 30,

as shown in Figure 3, for example, is provided` with a multiplicity of perforations 32, so that steam is directed both externally and internally upon any material resting upon the apex member In addition, a steam line 33 is provided extending through the ring member l8 and communicating with a multiplicity of upwardly directed outlets 34 in the ring member. In this manner, steam is directed downwardly and up- ,wardly, as well as outwardly upon any material disposed upon the apex member and presents substanti ally an atmosphere of steam. The steam is preferably of such pressure that it will not force any material ofi of the perforated or grid-like apex member. The perforations 32' are directed downwardly, as shown in Figure 3 and Figure 6, so that the loose material cannot find its way into the steam chest.

The apex member 30 is detachably supported upon an intermediate conical member 35 which, in turn, is detachably supported upon a conical extension 38 separable from or integral with the base of the furnace. Between the several sections 30, 35 and 36 forming the conical table, there is provided a suitable seal and insulator, for example, said indicated generally at 31 and it is to be noted that the several sections are joined by an interfitting relation, that is, the section 30 has a projection 38 fitting in the insulated groove 39 in the intermediate section 35 and the sections 35 and 36 are similarly constructed.

It is to be noted that the ring member !8 terminates substantially at the joint between the apex member 39 and the intermediate supporting section 35 of the conical table. The area of the conical table between the apex thereof and the ring member !8 constitutes the reaction zone of the apparatus and the proximity of the inner edge of the ring member and the wall of the conical member is controlled, so that when a layer` oi material is on the conical table and moving downwardly thereover, it cooperates with the ring member to substantially segregate or exclude the reaction zone from the remainder of the apparatus.`

Referring to Figure 2, the furnace is extended, as shown at 40, to provide the outlet 20 and the hasin formed by the extension communicates with the openings !9 in the bottom wall of the chamber ll. In one form of the invention, a molten mass o-f the reaoted material is disposed in the furnace below the ring member !8 and above the level of the openings !9 in' the bottom of the chamber II so that this bath will further act as a seal to prevent theentrance of contaminating influences. The products of' combustion pass through the conduit 4! above the level of the molten bath to the stack 42 where they are withdrawn, while the molten metal overfiows through the outlet 20 to-theconveyor 2l.

As a. further modification of the Construction, it is sometimes desirable to ro-tate the apex member 30 and referring to Figure 4, I have 'illustrated the apex member'as provided with an integral, downwardly extending sleeve 45. This sleeve is adapted to be rotated about the tube l5' by means of gearing 46. At its upper end, the tube l5' .is enlarged as at 41 to form an upper hearing, while at the lower end thereof there is fixed a plate member 48 forming the lower bearing. The sleeve 45 is provided with a plurality of spaced openings 49 opening at the top into steam chest 31 and at the bottom into the enlarged end of the sleeve in communicating relation with a circular groove 50 formed in the plate 48. Communicating with the groo-ve is a steam line 5I. steam from the line 5| supplies the groove 50 and this, in turn, Supplies the openings 49'in the sleeve 45 'With steam for introduction into the steam chest 3l. The enlarged end of the lower end of the sleeve is rmly Secured to the plate 48 by means of a ring 52, which engages a flange 53-0n the base of the sleeve and is bolted or drawn upon the plate 48 and the fiange 53 by means of the bolts 54. A suitable packng 55 is interposed between the plate 48 and the bottom surface'of the enlarged end of the sleeve to form a steam seal 'and a similar gasket 55 is disposed between the sleeve and the adjacent wall of the tube I5'. i In order that the apex member 33 may be easily rotated, I preferably provide suitable hearing surfaces and 51 between the bottom of the apex member and the adjacent upper surfaceof the intermediate member 35 and interposesuitable roller bearings 58 between the s urfaces. In this Construction the steam line Z'Lextends up through the shaft 26 of the feed screw to preheat the mixture, and through a spider 59 supported upon the enlarged bearing end.41 of the tube I5'., This spider carries a distributing head 60 for `the steam nozzles 28 The purpose of providing a rotary apex member is to afiord, ,in some cases, a more even disthe downwardly directed openings or perforations c 32. The purpose of this is to control the feed of the material by providing a series of retarding obstructions indicated at 62 which are effective when the apex member is not rotated, but are particularly useful where the apex member is rotated and in a direction contrary to the direction in which 'the spiral is formed. That is, the spiral Construction will afford a means of retarding and hence controlling the downward flow of the reaction ingredients, so that, for some purposes, the reaction may be suitably prolonged.

In Figures 7 and 8, the apex member 63 is provided with a spiral vane 64 so that when the member is rotated clockwise, the mixture being reacted is fed downwardly at a controlled rate to assure proper reaction as well as'distributed as a layer and subjected to agitation.

In Figure 9, the reacted materials pass directly from the conical table to a suitable hopper 65, the table being extended to form a chute 66 and allow free and uninterrupted drop of the reacted.: materials into the hopper. In other respe cts, the apparatus is similar to that shown and described in connection with the other views of the clrawings and sus-ceptible to similar modifination. It is to be noted that the reaction zone and chute are segregated from products of combustion so that contamination of the reacted mass is avoided.

While I have shown the mixture as moving downwardly through the reaction zone, it may be reacted while traveling in a horizontal plane or even upwardly. The continuous downward movement as shown is preferred.

Also while I have described means for feeding the mixture upwardly through the cone and distributing the mixture at the apex thereof, a suitable chute, tube or trough may be provided extending through the top of the furnace n* and heating chamber I! or through the side walls thereof, and delivering metered quantities of the mixture to the apex of the cone 30 for continu-' ously forming and presenting a suitable layer of the mixture to be reacted.

The method Broadly, and re ferring to Figure 1, the solid constituents of the batch are fed through the trough 16 and the opening or tube l5' at a controlled speed and in a controlled quantity, so that upon being ejected at the apex of the conical table, they spread out and form as a thin layer thereon. At the same time, steam is introduced .and a temperature is maintained within the reaction Zone of about 1500 F. This is representative for the batch above mentioned and is subject to variation up or down, as the case may be, dependent upon the constituents and their percentage relation in the batch. The reaction zone is described by the upper surface of the ring member and the surface portion of the conical table extending thereabove, in association with the upper part of the chamber l l dened by the ring member and the top of the chamber. The material will move down the conical surface and the speed of its downwardmotion is controlled by the speed of the feed in the tube l5' and also by such means as the rotatable apex member, and the spirally formed or Vaned apex members, heretofore described. Preferably, conditions are so maintained that the reaction between the solid constituents and the steam is complete and no free sodium` chloride is carried with the reacted mass past or below the ring member !8. The reaction results in the formation of a reacted mass containing calcium silicate and sodium silicate, together with complex or poly-silicates and free silica. The plasticity or liquidity of the reacted mass will be governed by the temperatures and the speed of feed, i. e., the time period allowed for reaction, but usually the reacted mass is plastic i. e., molten or semi-molten at the conclusion of the reaction. In this state, of course, it is possessed of innumerable pores, holes, voids and cells. It is to be noted that the reaction is carried out with exclusion of products of combustion from the burners [2 by reason of the ring member IS, which is disposed' in close proximity to the wall of the conical member, so that the layer of material forms a seal against such contaminating influences and this seal is also aided by the bath level as shown in Figure 2 or the construction shown in Figure 9. The distance between the inner diameter of the ring member and the wall of the conical table may be adjustable as heretofore described and may be used in some cases to regulate the thickness of the layer formed upon the conical table.

During the reaction hydrogen chloride gas is formed and since the chamber H is free of contaminating influences, this hydrogen chloride is recovered through the stack !3 in substantially pure state and constitutes a valuable by-product.

Referring to Figures 1 and 2, the mixture is continuously discharged upon the apex member and continuously moves down the surface thereof, while being subject to the desired conditions of reaction. v

It will be noted that the relatively thin layer disposed upon the surface of the apex member is subjected to an atmosphere of steam provided by the outlets 28, 32 and 34. Since the layer is relatively thin and the steam is supplied thereto upon both sides, a. very complete and speedy reaction is afforded. The solid ingredients of thebatch .are finely divided, assuring an intimate reactive relation between them; the introduction of the steam throughout the relatively thin layer assures that the reaction will be completed under the predetermined conditions of speed of feed of the mixture, relative inclination of the conical table, or such feeding means as the rotatable apex member with or without a spiral surface or a vaned surface, by the time the reacted mass reaches the ring !3.

Referring to Figures 1 and 2, after the mass passes the ring [8, it encounters the bath 63 carried in the bottom of the furnace and which overflows from the basin w. This bath initially is made by melting glass, but as the reaction progresses, it becomes a bath of the reacted materials. The temperature of this bath is considerably'elevated, in the present instance, being at a temperature of about 2300 F.-24GO F. or high enough to 'maintain the reacted material molten. Upon introduction of the reacted material from the conical table to the bath, the reacted material assumes'the molten state and will overfiow from the outlet 20. It is to be noted that the level of the molten bath extends above the top of the openings ne in the bottom wall of chamber I l, so as to form a thorough seal against the entrance of combustion gases or other containinating influences into the reaction zone.

The molten reactecl material issuing from the outlet 20 is received upon the conveyor 2 i, where it is cooled to a frit and fed to the orusher 22. In this crusher, the frit is finely ground or subdivided and mixed. This finely divided mixture is now ready to be converted into complete glass simply by introduction to a glass melting furnace and heated to a temperature of: about 2700 F. By reason of the cooling and crushing step accompanied by a mixing of the crushed frit, I am enabled to 'obtain a high quality homogenized glass.

The melting furnace may be equipped with means for forming bottles and other containers, sheets and a variety of glass articles.

Moreover, the furnace o may be connected integrally with or otherwise communicate with the melting furnace, so that the molter reacted mass may be continuously or intermittently fed to the melting furnace, and there refined into glass and formed into glass .articles preferably as a. continuous operation.

I have generally described the method employed by me for the manufacture of glass, utilizing sodium chloride instead of sodium carbonate. The

use of sodium chloride assures a substantial economy in the cost of raw materials and the method herein set forth being devoid of any complicated procedure or apparatus is conducted at so low a cost as to be thoroughly commercially feasible. It is this discovery which I have made in both method and apparatus that assures the production of a high quality glass at a substantial reduction in operating costs.

The Construction illustrated in Figures 4,' 5 and 7, namely the use of a rotary apex member, a spirally ormed or a spirally vaned apex member or a spirally formed or spirally vaned rotatable apeX member enables the distribution of the layer of material upon the apex member and its flow to be controlled for certain purposes and is highly eicient in the production of the high quality product of this invention. For example, the rotary apex' member will assure a very even distribution, as well as afford some agitation of the constituents to promote their complete reaction .and control the rate of downward flow. The spiral or spiral vaned apex members likewise assure an intimate relaticn between the solid ingredients and their reaction with the steam and each other and, as explained above, will control the continuous downward movement of the layer.

Referring to Figura 9, the reacted mass as discharged past the ring member !8, is immediately and directly cooled to a solid frit. This frit in its cooled state is recovered from the hopper 65 and suitably ground and then converted to complete glass, as previously described.

In certain cases, as where I desire to produce an acoustic or insulating material, the molten material issuing from the opening 20 is molded in the form of bricks or slabs. If desired, the plasticity of the bath may be changed for the particular molding operation; The reacted mass as it issues from the opening 20, is in unrefined state and, therefore, contains enumerable bubbles, holes, voids and similar imperfections. These, of course, are present in the molded article and afford the desired acoustic and insulating properties. If desired, the cooled frit from the conveyor ZI may be remelted and then molded, providing, of course, that the melting does not so refine the glass as to render it devoid of the required number of pores.

Such insulating or acoustic products may be obtained also by immediately molding the relatively plastic mass issuing from the reaction chamber past the ring member s. For example, in accordance with the method shown in Figure 9. If the reacted mass does not have the required plasticity as it passes under the ring member l8, I can direct burners upon the lower wall 61 of the 'charged from the conveyor.

heating chamber, so as 'to obtain any desired plasticity and the plastic mass may then be immediately molded. This product, likewise in the form of bricks ar slabs, is useful for acoustic or insulating purposes, and is characterized by enumerable pores, openings and holes. i

In connection with the various apparatus illustrated and described, it is to be understood that they are co'nstructed of suitable heat resisting material, either metal or argillaceous compounds and that the heating chamber I l is suitably lined to be resistant to the hydrochloric acid gas, as well as high temperatures. The conical table likewise is resistant to both high temperatures and chemical action of the reaction con stituents and the reaction products.

While I have described the present invention as concerned with the manufacture of glass, it is to be understood that the process and apparatus here disclosed is equally applicable to the manufacture of. sodium silicate from sodium chloride, sand and steam. In carrying out this process the temperature of the heating chamber is maintained at about 950 to 1600 F. to insure reaction of the silica with the sodium and the production of hydrochloric acid gas. The proportions of ingredients will be, of course, worked out in the usual manner to produce a complete reaction and the sodium silicate fiows down the conical table, for example, either to the bath, or into a hopper as shown in Figure 9.

I produce from the frit prepared in accordance with this invention, a further type of molded product wherein the ground frit is placed in a mold and heated at a temperature just sufiicient to melt the surface. Thus in the case of a brick, there will be formed a product having a smooth or roughened continuous outer surface and a porous interior composed of the granules of the frit in their original state. For producing this type of product, the molds may be carried on -a conveyor, and the frit subjected to a temperature of about 1500 to 2000 for a brief period to form the surface skin, whereupon the product is then suitably annealed in the mold, and dis- In some cases the product is removed from the mold before annealing. e

In order to avoid shrinkage of the product, it is in some cases desirable to spin or rotate the mold Whereby, due to centrifugal force, the resultant product will undergo no substantial change in its outer dimensione While interiorly, therewill be a hollow core.

While I refer to the frit of the present invention as useful in manufacturing this type of article, it is to be understood that glass from any source may beground and similarly molded and treated to produce the same product. Thus ordinary glass cullet is ground and placed in a mold and the material subjectedto a heating such as will form the surface skin, annealed within or without the mold. The 'mold may or may not be spun as required.

Another product consists in spraying the ground frit or ground glass from any source with sodium silicate in its adhesive state and thereafter pressing, molding or otherwise forming the coated ground frit or glass into articles of any desired shape with suitable hardening 'of the binder. Such articles, of course, may be formed with a surface skin in the manner heretofore disclosed if desired.

I claim:

The method of making glass comprising mixof sodium and calcium and complex or polysilicates in molten or semi-molten state, continuously collecting the reacted mass aas formed,

and cooling the same to a rit capable of being converted to glass by heating.

WILLIAM STANLEY RENDALL. 

